US1417007A - Island - Google Patents
Island Download PDFInfo
- Publication number
- US1417007A US1417007A US1417007DA US1417007A US 1417007 A US1417007 A US 1417007A US 1417007D A US1417007D A US 1417007DA US 1417007 A US1417007 A US 1417007A
- Authority
- US
- United States
- Prior art keywords
- plates
- acid
- electrolyte
- battery
- specific gravity
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000002253 acid Substances 0.000 description 16
- 239000003792 electrolyte Substances 0.000 description 15
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 12
- 230000005484 gravity Effects 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 11
- 239000001117 sulphuric acid Substances 0.000 description 11
- 235000011149 sulphuric acid Nutrition 0.000 description 11
- 239000000725 suspension Substances 0.000 description 8
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 6
- 239000008119 colloidal silica Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000007599 discharging Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 239000011148 porous material Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- OSWPMRLSEDHDFF-UHFFFAOYSA-N methyl salicylate Chemical compound COC(=O)C1=CC=CC=C1O OSWPMRLSEDHDFF-UHFFFAOYSA-N 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000007784 solid electrolyte Substances 0.000 description 2
- 101100345589 Mus musculus Mical1 gene Proteins 0.000 description 1
- 241000220010 Rhode Species 0.000 description 1
- 239000011280 coal tar Substances 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011244 liquid electrolyte Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229960001047 methyl salicylate Drugs 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- -1 three parts Substances 0.000 description 1
- 239000009637 wintergreen oil Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/12—Construction or manufacture
- H01M10/128—Processes for forming or storing electrodes in the battery container
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/08—Selection of materials as electrolytes
- H01M10/10—Immobilising of electrolyte
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Definitions
- My invention relates to the process of making or setting up electric storage batteries having lead plates and a solid electrolyte of the general character described in my pending application Serial No. 830,893 filed October 15, 1919.
- Said solid electrolyte is preferably formed of colloidal silica, with possible admixture other uaterial, and sulphuric acid in suspension in said silica, which silica has been produced in situ by pouring a mixture oi: liquid silicate of soda and dilute sulphuric acid into the battery cell. In a few minutes after such mixing and pouring, a portion of the acid combines with the silicate of soda to form a large volume of colloidal silica and the residual acid solution which remains in suspension on the highly porous mass of silica is capable of electrolytic action on the lead plates in the usual way when the battery is charged and discharged.
- v present invention is based on the discovery that to produce an entirely satisi ac tory battery of this kind it is necessary to prepare the plates by several preliminary charges and discharges in a separate acid electrolyte before the silicate of soda and acid solution is poured around the plates, and that in such preparation of the plates they should be finally charged or discl'iarged. to a point that will reduce the sulphuric acid in their pores to a specific gravity substantially equal to that of the residual acid which will occur in the battery filling after the solid filling has been introduced and the reaction producing the colloidal silica has been completed.
- I may state the following: I
- any negative plate reads less than .10 volts, it lacks capacity and should be overcharged at a low rate in order not to injure the positives.
- the density of the electrolyte in all cells should be equalized belore discharging. In most batteries which are used for vehicles or starting and lighting, the proper density should be 1.300 specific gravity at a temperature of Fahr.
- each cell. shows the proper voltage and both positive and negative cadmium readings are correct and the electrolyte is of the right density, the battery is fully charged, and in proper condition. The battery should then be discharged until the said electrolyte has a specific gravity of about 1.200.
- liquid electrolyte is then poured out and a mixture introduced which on setting around the plates in each cell will produce the desired colloidal mineral filling, holding in suspension a residual sulphuric acid of a specific gravity of about 1.200.
- my process commercial silicate of soda mixed with about three quarters of one per cent by volume of methyl salicylate, commonly called synthetic oil of Wintergreen and an equal amount of a suitable liquid coal tar product, such as the material known commercially as Wests disin fectant.
- This mixture is then diluted with three (3) volumes of water, and after the battery plates have been treated as above described, the diluted mixture is thoroughly mixed with live (5) volumes of sulphuric acid of a specific gravity of 1.400 and the final mixture poured into the cells around the plates.
- the solid filling so formed is of? a stiff, gelatinous consistency and will not crack or break up under standard conditions of use of the battery. There is a slow evaporation of the water content which should be rcmedied by occasionally pouring a little fresh water into the mass which tends to become too dry and hard by slow evaporation of the li uid contents.
- the herein described method of forming electric storage batteries With a solid filling surrounding lead plates and holding the electrolyte in suspension which comprises the following steps: first, charging and discharging the plates in a free solution of acid electrolyte until the acid in their pores is of a predetermined specific gravity Within the standard battery range; second, removing the free solution oi acid electrolyte and substituting a fluid mixture which on the completion of internal chemical reactions will form a solid mass holding .in suspension a residual. portion of the same acid electrolyte of substantially the same predetermined specific gravity.
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Secondary Cells (AREA)
Description
UNITED STATES HORACE M. WILLIAMS, 0]? PROVIDENCE,
RHODE ISLAND, ASSIGNOR T0 ELEOTBOL MANUFACTURING- GOMPANY, A CORPORATION OF RHODE ISLAND.
PROCESS OF MAKING ELECTRIC STORAGE BATTERIES,
No Drawing.
- tion.
My invention relates to the process of making or setting up electric storage batteries having lead plates and a solid electrolyte of the general character described in my pending application Serial No. 830,893 filed October 15, 1919.
Said solid electrolyte is preferably formed of colloidal silica, with possible admixture other uaterial, and sulphuric acid in suspension in said silica, which silica has been produced in situ by pouring a mixture oi: liquid silicate of soda and dilute sulphuric acid into the battery cell. In a few minutes after such mixing and pouring, a portion of the acid combines with the silicate of soda to form a large volume of colloidal silica and the residual acid solution which remains in suspension on the highly porous mass of silica is capable of electrolytic action on the lead plates in the usual way when the battery is charged and discharged.
v present invention is based on the discovery that to produce an entirely satisi ac tory battery of this kind it is necessary to prepare the plates by several preliminary charges and discharges in a separate acid electrolyte before the silicate of soda and acid solution is poured around the plates, and that in such preparation of the plates they should be finally charged or discl'iarged. to a point that will reduce the sulphuric acid in their pores to a specific gravity substantially equal to that of the residual acid which will occur in the battery filling after the solid filling has been introduced and the reaction producing the colloidal silica has been completed. As an example of the best method at present known to me in which my invention may be carried out, I may state the following: I
Fully charge the battery at the rate recommended by the manufacturer using the standard sulphuric acid solution as the electrolyte until the voltage reaches 2.55 per cell.
Take a cadmium reading of both positive and negative plates. These readings should Specification of Letters Patent.
Patented May 23, 1922.
Application filed August 19, 1920. Serial No. 404,667.
be 2.40 to volts for the positive plates and .10 to .15 volts for the negative plates.
Ii? any negative plate reads less than .10 volts, it lacks capacity and should be overcharged at a low rate in order not to injure the positives.
If the negatives do not improve by such treatment discharge the battery at the 4 hour rate until voltage drops to 1.80, per cell, and recharge It is advisable to empty the cells and use fresh acid before this discharg ing, as impurities in the electrolyte will cause trouble with the plates.
The density of the electrolyte in all cells should be equalized belore discharging. In most batteries which are used for vehicles or starting and lighting, the proper density should be 1.300 specific gravity at a temperature of Fahr.
If. after re-charging. each cell. shows the proper voltage and both positive and negative cadmium readings are correct and the electrolyte is of the right density, the battery is fully charged, and in proper condition. The battery should then be discharged until the said electrolyte has a specific gravity of about 1.200.
In discharging. if a ea-k cell drops "to 1.8 volts before the rest, cut it out and continue discharge. The weal: cell will receive an overcharge when the battery is recharged, which may correct the trouble.
The liquid electrolyte is then poured out and a mixture introduced which on setting around the plates in each cell will produce the desired colloidal mineral filling, holding in suspension a residual sulphuric acid of a specific gravity of about 1.200. I prefer to use in this portion o1 my process commercial silicate of soda mixed with about three quarters of one per cent by volume of methyl salicylate, commonly called synthetic oil of Wintergreen and an equal amount of a suitable liquid coal tar product, such as the material known commercially as Wests disin fectant. This mixture is then diluted with three (3) volumes of water, and after the battery plates have been treated as above described, the diluted mixture is thoroughly mixed with live (5) volumes of sulphuric acid of a specific gravity of 1.400 and the final mixture poured into the cells around the plates.
In a few minutes all the silicate of soda in the solution combines with its proper proportion of the acid forming a voluminous mass of colloidal silica, and a relatively small amount of sodium sulphate. The colloidal silica fills the cell and retains in suspension the surplus of the sulphuric acid which Will have a specific gravity of a little over 1.200 or almost exactly the same that of the acid existing in the pores of the plates. A perfectly balanced battery is thus produced.
Upon fully charging the battery so formed it will be found to develop substantially the same efiiciency and capacity as though it had a liquid acid electrolyte, and to be devoid of the disadvantages due to the corrosive action of the spraying, slopping and creeping liquid acid electrolyte. Also the plates of batteries with this filling are practically proof against snlphating and shedding, and have a long life under the most trying conditions of use.
The solid filling so formed is of? a stiff, gelatinous consistency and will not crack or break up under standard conditions of use of the battery. There is a slow evaporation of the water content which should be rcmedied by occasionally pouring a little fresh water into the mass which tends to become too dry and hard by slow evaporation of the li uid contents.
Iaving described my invention, I claim:
1. The herein described method of forming electric storage batteries With a solid filling surrounding lead plates and holding the electrolyte in suspension, which comprises the following steps: first, charging and discharging the plates in a free solution of acid electrolyte until the acid in their pores is of a predetermined specific gravity Within the standard battery range; second, removing the free solution oi acid electrolyte and substituting a fluid mixture which on the completion of internal chemical reactions will form a solid mass holding .in suspension a residual. portion of the same acid electrolyte of substantially the same predetermined specific gravity.
2. The herein described method of forming electric storage batteries with a solid filling surrounding lead plates and holding a sulphuric acid electrolyte in suspension, which comprises the following steps? first, changing and discharging the plates in a free solution of sulphuric acid of original standard battery specific gravity until the acid in the pores of the plates hasa specificv gravity approximating 1.200 second, removing said 'lrec electrolyte and substituting a mixture by volume of liquid. silicateof soda, one part, water, three parts, and sulphuric acid of 1. .1100 specific gravity, five parts, whereby after chel'nical combii'lation oi? the silicate of soda with a portion of the acid to form a voluminous mass of colloidal silica of gelatinous consistency, there will remain in suspension in said mass a residual content of sulphuric acid of approximately 1.200 specific gravity, as the active electrolyte for the battery so produced.
HORACE M. WILLIAMS.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1417007A true US1417007A (en) | 1922-05-23 |
Family
ID=3401480
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US1417007D Expired - Lifetime US1417007A (en) | Island |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1417007A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3930881A (en) * | 1974-07-22 | 1976-01-06 | Nl Industries, Inc. | Immobilized battery electrolyte |
| WO1986007496A1 (en) * | 1985-06-13 | 1986-12-18 | Otto Jache | Lead accumulator with a thixotropic gel as electrolyte, and production method |
| US4863816A (en) * | 1987-07-29 | 1989-09-05 | C&D Power Systems, Inc. | Alkali metal polysilica gel electrolyte lead-acid battery and method for making the same |
| US4889778A (en) * | 1987-07-29 | 1989-12-26 | C & D Power Systems, Inc. | Alkali metal polysilica gel electrolyte lead-acid battery and method for making the same |
| US5593796A (en) * | 1992-02-10 | 1997-01-14 | C & D Charter Power Systems, Inc. | Recombinant lead-acid cell and long life battery |
-
0
- US US1417007D patent/US1417007A/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3930881A (en) * | 1974-07-22 | 1976-01-06 | Nl Industries, Inc. | Immobilized battery electrolyte |
| WO1986007496A1 (en) * | 1985-06-13 | 1986-12-18 | Otto Jache | Lead accumulator with a thixotropic gel as electrolyte, and production method |
| US4929251A (en) * | 1985-06-13 | 1990-05-29 | Otto Jache | Method for producing lead accumulator with thixotropic gel |
| US4863816A (en) * | 1987-07-29 | 1989-09-05 | C&D Power Systems, Inc. | Alkali metal polysilica gel electrolyte lead-acid battery and method for making the same |
| US4889778A (en) * | 1987-07-29 | 1989-12-26 | C & D Power Systems, Inc. | Alkali metal polysilica gel electrolyte lead-acid battery and method for making the same |
| US5593796A (en) * | 1992-02-10 | 1997-01-14 | C & D Charter Power Systems, Inc. | Recombinant lead-acid cell and long life battery |
| US5645957A (en) * | 1992-02-10 | 1997-07-08 | C & D Charter Power Systems, Inc. | Lead-acid battery having a cover extending beyond a jar |
| US5695891A (en) * | 1992-02-10 | 1997-12-09 | C & D Charter Power Systems, Inc. | Battery thermal management system |
| US5851695A (en) * | 1992-02-10 | 1998-12-22 | C & D Technologies, Inc. | Recombinant lead-acid cell and long life battery |
| US6667130B2 (en) | 1992-02-10 | 2003-12-23 | C&D Charter Holdings, Inc. | Recombinant lead-acid cell and long life battery |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| SE457036B (en) | SEATED IN PREPARATION OF A BLYACKUMULATOR WITH A TIXOTROPT GEL AS ELECTROLYTE AND BLYACKUMULATOR MADE AS SET | |
| JP2690540B2 (en) | Lead acid battery having electrolytic solution obtained by gelling alkali metal polysilica and method for manufacturing the same | |
| US1417007A (en) | Island | |
| US2938063A (en) | Storage battery active material | |
| US3194685A (en) | Method of manufacturing storage battery electrode active material | |
| US4687718A (en) | Method of making a sealed lead-acid battery with a gel electrolyte and sealed lead-acid storage battery made according to this method | |
| US3556860A (en) | Storage battery and electrolyte precursor therefor | |
| US3271199A (en) | Solid acid storage battery electrolyte | |
| US2759037A (en) | Dry charged batteries | |
| US3839089A (en) | Water activated lead acid storage battery cell having dry discharged electrodes | |
| US1634850A (en) | Electric battery and process of making the same | |
| US2422437A (en) | Method of preparing paste for electric storage battery plates | |
| US20010051301A1 (en) | Process for producing an industrial electrolyte for lead storage batteries in the form of a thixotropic gel | |
| JP4441934B2 (en) | Method for producing lead-acid battery | |
| US1478708A (en) | Process of manufacturing storage batteries | |
| US724619A (en) | Electric accumulator. | |
| US1496725A (en) | Dry storage battery | |
| US3418166A (en) | Alkaline storage cell having silicate dissolved in the electrolyte | |
| JPS60193274A (en) | Improved liquid for car battery and car battery improving method by using improved liquid | |
| US1468259A (en) | Storage-battery practice | |
| US1879639A (en) | Composition of matter | |
| JPS60211777A (en) | Manufacture of battery | |
| JPH0883622A (en) | Sealed lead acid battery | |
| US1668741A (en) | Method of making storage batteries | |
| JPS6313261A (en) | How to charge a lead battery |